Tangential velocity of the impeller at inlet
GO
Tangential velocity of impeller at outlet
GO
Impeller radius at inlet given inlet tangential velocity
GO
Work done per second in terms of torque and angular velocity
GO
Work done per second per unit weight of liquid
GO
Work done per second if the flow at inlet is not radial
GO
Work done per second per unit weight of liquid if the flow at inlet is not radial
GO
Volume of liquid at inlet
GO
Manometric head in terms of static head and losses in pipes
GO
Manometric head in terms of head imparted by the impeller and loss of head in the pump
GO
Manometric head in terms of total head at outlet and inlet of the pump
GO
Manometric efficiency in terms of velocities
GO
Tangential velocity of the impeller at inlet in terms of angular velocity and impeller radius
GO
Tangential velocity of the impeller at outlet in terms of angular velocity and impeller radius
GO
Volume of liquid at outlet
GO
Manometric head in terms of static head, friction losses in suction and delivery pipes
GO
Manometric head in terms of head imparted by the impeller if loss of head in the pump is zero
GO
Overall efficiency in terms of manometric, volumetric and mechanical efficiencies
GO
Minimum speed for starting a centrifugal pump
GO
Tangential velocity given speed ratio
GO
Flow velocity given flow ratio
GO
Flow velocity at inlet given volume of liquid
GO
Flow velocity at outlet given volume of liquid
GO
Outlet diameter of impeller in terms of speed ratio, manometric head and impeller speed
GO
Manometric head given outlet impeller diameter, impeller speed and speed ratio
GO
Least diameter of impeller
GO
Diameter of suction pipe
GO
Diameter of delivery pipe
GO
Leakage of liquid given volumetric efficiency and discharge
GO
Thoma's cavitation factor
GO
Net positive suction head
GO
Suction specific speed
GO
Thoma's cavitation factor in terms of net positive suction head
GO